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Publication numberUS6379414 B1
Publication typeGrant
Application numberUS 09/559,845
Publication dateApr 30, 2002
Filing dateApr 27, 2000
Priority dateApr 28, 1999
Fee statusPaid
Also published asCA2306585A1, CA2306585C, DE19919233A1, DE19919233C2, DE50015943D1, EP1048634A2, EP1048634A3, EP1048634B1
Publication number09559845, 559845, US 6379414 B1, US 6379414B1, US-B1-6379414, US6379414 B1, US6379414B1
InventorsUlrich Kleine-Kleffmann, Ludger Waldmann, Frank Wolf
Original AssigneeKali Und Salz Gmbh
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Process for producing pressed fertilizer granulates
US 6379414 B1
A process is for the production of potash fertilizer granulates which have a stable shelf life also at high relative air humidities. This granulate contains an additive in the form of magnesium oxide and/or calcium oxide in a fine powder form, which is added by metering in prior to the compacting step. The result is a high final bursting strength even if the granulate is stored in a wet climate.
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What is claimed is:
1. A process for producing humidity resistant pressed granules of potash fertilizer comprising
(a) mixing dry fine potash salt and an additive powder selected from the group consisting of dry finely, ground magnesium oxide, calcium oxide and a mixture of MgO and CaO, to form a dry mixture;
(b) pressing this dry mixture into the shape of barnacles pressed product; and
(c) processing this pressed product into granules.
2. The process according to claim 1, comprising
metering in the additive powder uniformly into the fine salt prior to pressing and producing a homogeneous mixture.
3. The process according to claim 1, comprising
adding the additive by metering in a total amount of from 0.2% by weight based on the dry total weight of the granulate.
4. The process according to claim 1, comprising adding the additive by metering in a total amount of from 1% to 1.5% by weight based upon the total weight of the granulate.
5. The process according to claim 1,
wherein the calcium oxide additive powder is burnt lime.
6. The process according to claim 1,
wherein the mixture of CaO and MgO additive powder is burnt dolomite.

1. Field of the Invention

The present invention relates to the compacting of potash salt for the production of fertilizer granulates, and in particular of potassium chloride. These potash salts were obtained by treating raw mixtures or single salts by way of crystallization or flotation.

2. The Prior Art

Potash salt granulates are usually produced by build-up and press granulation. In the build-up granulation process, moist salt from the dehydration stage is mixed with dry salt of the finest type (re-circulated dust) as well as auxiliary granulating agents, and adjusted with water or off-lye to the required granulating moisture. The salt is subsequently compacted in drums to produce round granules. The “green” granules so obtained are subsequently dried.

In the press granulating process, fine product that has already been dried is pressed on presses (e.g. roll presses) into the shape of so-called “barnacles” or shells with a thickness of a few millimeters. These shells are thereafter subjected to a grinding and screening process. The coarse screening product is the finished product, whereas the undersized grain is re-circulated (Ullmann's Encyclopedia of Technical Chemistry, 4th edition, volume 13, page 471; Verlag Chemie, Weinheim). No auxiliary granulating agents are added during compacting. The resulting pressed granulates are solid and have a stable shelf life at the normal medium humidity values which are found at median latitudes.

At high relative air humidity values which are found, for example in tropical countries, it is found that the pressed granulate exhibits increased water absorption. This may furthermore lead to decomposition of the grain, to an increase in the amount of the fine component, and to hardening of the product.

Decomposition phenomena which may be occurring, for example in connection with salt lick stones for animal fodder can occur under the influence of the weather outdoors. These problems are dealt with according to U.S. Pat. No. 2,599,436, among others, as follows. The salt component, which is sodium chloride, as a rule, is mixed with components of up to 6% MgO as well as up to 12.5% of an about 20% MgCl2 solution, and then hardened in molds.

Such a procedure is not possible in connection with the press granulation of potash fertilizer salts because such compacting is a dry process in which the compacting pressure plays the decisive role for the strength of the granulates. Furthermore, the required chemical quality of the fertilizer granulates would be impaired in an impermissible manner.


It is an object of the present invention to produce a pressed granulate which is solid and stable also under extreme climatic conditions such as high relative air humidity values and elevated outside temperatures, and which will not decompose even when stored over longer periods of time. At the same time, the required chemical quality of the salt to be granulated is not to be impaired.

It has now been found that the water absorption of a pressed granulate, for example of a 60-type potash salt fertilizer, from the ambient moist air can be suppressed. This suppression occurs if small amounts of magnesium oxide in the form of powder are added to the dry fine salt to be granulated. A dry mixture is then produced, which is then processed into granules according to known compacting methods.

It has been found, furthermore, that the compacted granulate produced in this way has a final bursting strength even under elevated air humidity values and temperatures that is a higher bursting strength than the one of a comparably pressed granulate not treated as defined by the invention. The effect can be observed also after longer storage periods at high relative humidities. The product remains granular and stable.

The positive effect can be observed in connection with all commercially available MgO-specifications.

In a preferred embodiment of the process of the invention, fine salt to be granulated such as a fine, dry KCl-crystallizate is obtained in a dissolution process or a flotation process. It is mixed with finely ground magnesium oxide, and the mixture is then pressed into the shape of barnacles (or shells) with application of the usual compacting pressures, for example on a roll press. These barnacles are subsequently ground and processed into granulate with the required grain size by the usual circulation processing procedure including classifying and separating. According to the invention, contents of 0.2 to 2 percent, by weight, preferably 1 to 1.5 percent by weight of dry MgO powder based on the dry amount of granulate are metered into the granulate. Higher contents lead to an insignificant improvement in the result which, however, bears no comparison with the attendant reduction in the content of valuable material in the final granulate.

The positive effect of the invention is developed in the same way if prior to the pressing step, preferably burnt lime in the form of powder, or burnt dolomite (CaO/MgO) are metered into the calcium oxide components. They are present in small amounts according to the invention. The process is not limited to the compacting of potassium chloride, but applicable for other potash salt fertilizers as well, for example also for potassium sulfate.


The present invention is further illustrated by reference to the following examples which are not to be deemed limitative of the invention in any manner thereof.


A commercially available magnesium oxide powder is metered prior to the compacting step on a roll press into a dry 60-type fine floatation salt. The amount of MgO is such that a content of 1.3% MgO by weight based on the total weight of finished granulate is produced in the continuous process of circulation granulation with screen separation. The MgO-quantity is evenly distributed upstream and downstream of the press by mixing processes in the aggregates.

The granulate so obtained is now stored and the absorption of moisture and the bursting strength are measured in the course of storage. The following results were obtained as compared to a granulate produced without the addition of MgO under the same conditions and are presented in Table 1.

Plant Test:
Added substance: Without MgO
Amount added: 1.3%
Start 0.1 0.1
Moisture absorption1, after
Moisture absorption1, after 1 d 2.5 1.0
Moisture absorption1, after 2 d 2.9 1.1
Moisture absorption1, after 4 d 3.4 1.2
Moisture absorption1, after 8 d 3.7 1.4
Bursting strength2 Start 51 55
Bursting strength2 1 d 27 55
Bursting strength2 2 d 25 46
Bursting strength2 4 d 24 47
Bursting strength2 8 d 21 40
1Weight increase in % during storage at 20° C., 70% rel. air humidity.
2Bursting strength in N/grain (fraction 2.5-3 mm)

The comparison of the measured values shows the improved results as defined by the present invention as the storage duration time in days (d) increases. Namely there is nearly a constant absorption of moisture in the granulate with MgO, versus the strongly rising absorption of moisture in the comparative granulate without MgO. The improved results as defined by the invention with respect to the development of the bursting strength is reproduced in the same way. The relatively high starting bursting strength remains intact with the granulate with MgO also after longer storage time in days, whereas a very large decrease in the bursting strength is seen with the comparative granulate without MgO.


The following Table 2 shows a comparison of the results produced by the present invention of a 60-type KCl-fine salt with MgO compacted under laboratory conditions, as well as of a compacted 60-type KCl-fine salt with CaO, with the MgO and CaO components each amounting to 1.5% by weight based upon the granulate total weight. This was compared to a granulate without this addition.

Laboratory Test:
Added substance:
Without 1.5% 1.5%
Moisture absorption1
After 1 d 2.3 1.0 1.4
2 d 3.1 1.2 1.4
4 d 4.1 1.3 1.5
8 d 5.2 1.3 1.5
Bursting strength2 Start 35 53 45
1 d 18 40 43
2 d 19 49 31
4 d 8 34 41
8 d 14 42 37
1Weight increase in % during storage at 20° C., 70% relative air humidity.
2Bursting strength in N/grain (fraction 2.5-3 mm)

The improved results as defined by the present invention is reproduced in the same way as according to Example 1. Specifically, it has to be noted that there is no significant difference between the positive effects of CaO and MgO. The time is in days (d).

While a few embodiments of the present invention have been shown and described, it is to be understood that many changes and modifications may be made thereunto without departing from the spirit and scope of the invention as defined in the appended claims.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2599436Aug 15, 1950Jun 3, 1952Int Minerals & Chem CorpSalt block
US3617237 *Dec 23, 1969Nov 2, 1971Mitsui Toatsu ChemicalsProcess for producing granular compound fertilizer
US3926609 *Apr 18, 1974Dec 16, 1975Kali & Salz AgGranular mgo-containing potassium salt fertilizers and process for their manufacture
US4101637 *Oct 29, 1975Jul 18, 1978J. R. Simplot CompanyReaction of phosphoric acid with lime, limestone, or dolomite
US4248617 *Mar 2, 1979Feb 3, 1981Mitsubishi Chemical Industries LimitedProcess for producing granular basic phosphate fertilizer
US4410350 *Mar 18, 1982Oct 18, 1983Martin Marietta CorporationProduction of pellets and pellet-containing fertilizer composition
US4946654 *Jul 26, 1988Aug 7, 1990Bayer AktiengesellschaftProcess for preparing granulates
US5264017 *Nov 23, 1991Nov 23, 1993Martin Marietta Magnesia Specialties Inc.Fertilizers
US5698007 *Aug 6, 1992Dec 16, 1997Akzo Nobel NvPretreating particulates with liquid spray of hydroxide ion source, mixing with water soluble polymer binder and water, agglomerating
US5743934 *Jul 5, 1996Apr 28, 1998Magic Green CorporationSoil conditioning agglomerates containing cement kiln dust
US5782951 *Feb 20, 1997Jul 21, 1998Western Industrial Clay Products, Inc.Particulate urea with finely divided inorganic material incorporated for hardness nonfriability and anti-caking
US6071325 *Jul 16, 1997Jun 6, 2000Akzo Nobel NvBy mixing with water particulate material such as iron ore, a binding amount of a water soluble polymer, and a binder enhancing amount of caustic to produce a mixture, and forming into agglomerates; efficiency, dry strength of agglomerates
DE3304303A1 *Feb 9, 1983Aug 9, 1984Ilseder Mischwerke IsvFertiliser and preparation of the fertiliser
JPH01157489A * Title not available
SU768450A1 * Title not available
Non-Patent Citations
1Ullmanns's Encyclopedia of Technical Chemistry, 4th ed., vol. 13, p. 471; Verlag Chemie, Weinheim.
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US8323371 *Aug 12, 2009Dec 4, 2012Kamalyte Resources Inc.Process for synthesizing a compacted product
US8685135 *Dec 3, 2012Apr 1, 2014Karnalyte Resources Inc.Process for synthesizing a compacted product
US20130031943 *Aug 6, 2012Feb 7, 2013Del FergusonCompacted muriate of potash fertilizers containing micronutrients and methods of making same
U.S. Classification71/61, 71/64.03, 71/31, 71/63
International ClassificationC05D11/00, C05D1/02, C05D1/00, B01J2/22, C05G5/00
Cooperative ClassificationC05D1/02
European ClassificationC05D1/02
Legal Events
Oct 2, 2013FPAYFee payment
Year of fee payment: 12
Sep 30, 2009FPAYFee payment
Year of fee payment: 8
Oct 7, 2005FPAYFee payment
Year of fee payment: 4
Apr 15, 2004ASAssignment
Effective date: 20011019
Owner name: K+S KALI GMBHKASSEL, (1) /AE
Aug 7, 2000ASAssignment